功夫在诗外——中专语文因材施教蠡测

随着中专生源的变化,中专语文因材施教势在必行。而因材施教绝不仅仅是技术层面上的问 题,而是内涵丰富。要求教师以人为本,用“心”教学,与时俱进。具体在情感态度、方式方法等方面要做到八 有:爱材之情;超材之能;识材之方;激材之术;练材之法;容材之量;管材之胆;育材之道。     

难处理硫化矿生物湿法冶金研究进展Ⅱ氧化机制、强化细菌浸出与生物反应器设计

着重评述了难处理硫化矿的矿物结构、性质及表面特征与各种电化学因素、细菌氧化机制与难处理硫化矿细菌强化浸出、浸矿基因工程菌以及生物反应器等方面的研究进展。指出缩短生物氧化周期长是细菌强化氧化研究的核心；将细菌繁殖和矿物氧化两个过程分开进行的“分离器-发生器”设备设计，是一值得推广的高效生物反应器。     

氧化铝生产中提高高压溶出效率的途径

通过对目前氧化铝生产中高压溶出进料量、机组运转率及技术指标状况的分析，指出了各项指标未达标的原因，提出了相应的改进措施。提出通过加强生产管理、优化操作条件可使溶出系统提高产能，对实际生产具有指导意义。     

高砷高硫金精矿固化焙烧-氰化浸出试验研究

介绍了高砷高硫金精矿矿物成分、固化焙烧-氰化浸出工艺条件，探讨了焙砂氰化浸出的机理。试验结果表明，金精矿经固化焙烧，焙砂氰化浸出时加入适量混合氧化剂(H2O2 KMnO4)和助浸剂G能显著提高金的浸出率，金浸出率为88．4％，砷、硫固化率均为90％。     

Immobilization of industrial waste in cement-bentonite clay matrix

Results of a series of experimental tests performed to determine the influence of matrix characteristics on the leaching mechanism of copper aluminum oxychloride immobilized into cement matrices are presented. The objective of this work was to investigate the leaching mechanism of copper as a constituent of copper aluminum oxychloride (‘CAOX’). Transport phenomena involved in the leaching of a waste material from a composite matrix into surrounding water were investigated using three methods based on theoretical equations: (i) diffusion equation derived for a plane source model, (ii) rate equation for diffusion coupled with a first-order reaction and (iii) the leaching data were also analysed by an empirical method employing a polynomial equation. These three methods are compared with respect to their applicability to the leaching data.     

永平铜矿低品位氧化矿堆浸技术的改进

分析了永平铜矿低品位氧化矿堆浸生产过程中存在的技术问题及问题产生的原因，考察了矿堆容重的改变及不同矿堆高度对溶液渗透速度的影响。详细介绍了对堆浸技术所进行的改进：(1)将原来前进式筑堆改为后退式筑堆；(2)在矿堆底部增加排水层；(3)变常规高层堆浸为硫酸熟化预处理薄层浸出；(4)实施分区喷淋与休闲轮换作业的布液制度。技术改进后，堆浸生产技术指标大为改观，取得了明显的经济效益。     

太湖地区麦季氮素淋失特征

通过排水采集器模拟试验,研究了太湖地区不同施肥水平下,麦作期间农田氮素淋洗特点。结果表明,麦季氮素渗漏损失以NO3--N为主,占总氮量的36.2%～99.1%,平均高达82.9%,NO3--N淋洗量随施肥量的增加而增加。不同施肥水平及肥料种类,对于NO3--N淋洗有着不同的影响,在试验的施肥水平下,麦作期间氮素淋失对地下水存在潜在污染。     

Study of Leaching of Multimetal Sulphides Through an Interdisciplinary Approach

The leaching of a real multimetal bulk concentrate cannot often be adequately understood on the basis of published literature on simpler and often ideal systems because the process is far too complex, Moreover, the data can become ambiguous in the absence of adequate information on raw materials. Thus any process development work requires a thorough knowledge of the raw material characteristics. This paper describes the use of an interdisciplinary study for a better understanding of ammonia leaching of multimetal sulphides. The techniques employed comprise of X-ray diffraction, thermal analysis, chemical analysis and microscopy.     

Extraction of aluminium as aluminium sulphate from thermal power plant fly ashes

Valuable metal extraction technology from thermal power plant fly ash is limited. In the present study, aluminium is extracted from fly ash as highly pure aluminium sulphate (>99.0%) by leaching with sulphuric acid, followed by pre-concentration and successive crystallization. Two types of fly ashes from different sources, i.e., Talcher Thermal Power Station (TTPS) and Vedanta Aluminium Company Limited (VAL) were chosen for comparative study on the extraction of aluminium as aluminium sulphate. The product is characterized by powder X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR) and thermogravimetric analysis (TGA). Purity of aluminium sulphate was also investigated by inductively coupled plasma–optical emission spectrometry (ICP–OES). The extraction efficiency of aluminium depends on the varied solid-to-liquid ratio (fly ash : 18 mol/L H₂SO₄, g/mL) and particle size of fly ashes. Physico-chemical analysis indicates that the obtained product is Al₂(SO₄)₃·18H₂O, having low iron content (0.08%).     

Primary beneficiation of tantalite using magnetic separation and acid leaching

Primary beneficiation was successfully performed prior to dissolution of manganotantalite （sample A） and ferrotantalite （sample C） samples obtained from two different mines in the Naquissupa area, Mozambique. Magnetic separation removed the majority of iron and titanium, whereas H2SO4 leaching removed a large portion of thorium and uranium in these samples. Analytical results indicated that 64.14wt% and 72.04wt% of the total Fe and Ti, respectively, and -2wt% each of Nb205 and Ta205 were removed from sample C （ferrotantalite） using the magnetic separation method, whereas only 9.64wt% and 8.66wt% of total Fe203 and TiO2, respectively, and -2wt% each of NbEOs and Ta2O5 were removed from sample A （manganotantalite）. A temperature of 50℃ and a leaching time of 3 h in the presence of concentrated HESOa were observed to be the most appropriate leaching conditions for removal of radioactive elements from the tantalite ores. The results obtained for sample A under these conditions indicated that 64.14wt% U3O8 and 60.77wt% ThO2 were leached into the acidic solution, along with 4.45wt% and 0.99wt% of Nb2O5 and Ta2O5, respectively.